EP0703193A2 - Rhombohedrisches Calciumcarbonat - Google Patents

Rhombohedrisches Calciumcarbonat Download PDF

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Publication number
EP0703193A2
EP0703193A2 EP95118361A EP95118361A EP0703193A2 EP 0703193 A2 EP0703193 A2 EP 0703193A2 EP 95118361 A EP95118361 A EP 95118361A EP 95118361 A EP95118361 A EP 95118361A EP 0703193 A2 EP0703193 A2 EP 0703193A2
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EP
European Patent Office
Prior art keywords
calcium carbonate
aging
heat
aged
particle size
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Granted
Application number
EP95118361A
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English (en)
French (fr)
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EP0703193B1 (de
EP0703193A3 (de
Inventor
Charles J. Kunesh
June D. Passaretti
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Minerals Technologies Inc
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Minerals Technologies Inc
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Application filed by Minerals Technologies Inc filed Critical Minerals Technologies Inc
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Publication of EP0703193A3 publication Critical patent/EP0703193A3/de
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/18—Carbonates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/18—Carbonates
    • C01F11/185—After-treatment, e.g. grinding, purification, conversion of crystal morphology
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/675—Oxides, hydroxides or carbonates
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/50—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by form
    • D21H21/52—Additives of definite length or shape
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/30—Particle morphology extending in three dimensions
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/54—Particles characterised by their aspect ratio, i.e. the ratio of sizes in the longest to the shortest dimension
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/60—Particles characterised by their size
    • C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/60—Particles characterised by their size
    • C01P2004/64—Nanometer sized, i.e. from 1-100 nanometer
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/12—Surface area
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values

Definitions

  • This invention relates to calcium carbonate having a specified crystal morphology, average particle size, particle size distribution and surface area, a process for producing this form of calcium carbonate product, and a method of use of the product as a filler material, for example, in papermaking, to improve the optical properties of the resulting paper.
  • Precipitated calcium carbonate has been used as a filler material in paper for many years.
  • Precipitated calcium carbonate has the advantage of being able to be produced in large quantity at relatively low cost. Therefore, it was decided to develop a form of precipitated calcium carbonate having a morphology which when used as a filler or extender in paper, affords the high level of brightness and opacity in the final paper product comparable to that achieved with the more expensive calcined clay and titanium dioxide filled papers.
  • One method of altering the morphology of a crystalline substance, such as precipitated calcium carbonate, in order to change its properties, is by Ostwald ripening or heat-aging.
  • Conventional heat-aging also known as Ostwald ripening, is a process whereby crystals, such as of calcium carbonate, initially at a higher internal energy state, and having a relatively small average particle size and relatively high phase solubilities, undergo a phase transformation by dissolving and redepositing on crystals at a lower internal energy state.
  • the process results in a final crystal product characterized by greater perfection of its crystal lattice structure, a narrower particle size distribution, greater degreee of particle discreteness and lower surface energy.
  • the procedure for conventional heat-aging of precipitated calcium carbonate produced by the reaction of calcium hydroxide and carbon dioxide is to endpoint the precipitated calcium carbonate synthesis at pH 8.0, screen the material to remove the impurities, and heat a 10% by weight solids slurry to the aging temperature (usually 80°C).
  • the pH of the system rises to approximately 10.5 due to the unreacted Ca(OH)2 in the slurry.
  • the aging reaction can be monitored by measuring the surface area of the calcium carbonate at hourly intervals.
  • Heat-aging of calcium carbonate with an initial morphology having a higher surface area and smaller average particle size to a final morphology having a surface area of from about 3 to about 15 m2/g and an average discrete particle size of from about 0.2 to about 0.9 microns typically takes extended periods of time ranging up to several hundred hours, depending in part on the degree of purity of the starting material and the aging temperature. The time required for heat-aging is inversely dependent on the purity of the starting material, the purer the material, the shorter the aging time required. Calcium carbonates containing impurities such as magnesium carbonate, at levels as low as several weight percent, require considerably longer heat-aging time to rearrange their morphologies.
  • the time required for heat-aging is also inversely dependent on the aging temperature; a longer time is required at lower temperatures, and a shorter time is required at higher temperatures.
  • large equipment volumes are needed, thus making this process uneconomical.
  • the primary objective of the present invention is a high opacifying, high brightness material that is applicable at a paper machine's wet end, size press, or coating stage and is competitive with current expensive fillers such as calcined clay and titanium dioxide, and a process for the rapid, cost effective production of such material in large quantity.
  • the present invention provides calcium carbonate of rhombohedral morphology, having a surface area of from about 3 to about 15 m2/g, an average discrete particle size of from about 0.2 to about 0.9 microns, wherein the discrete particles have an aspect ratio less than 2, and a particle size distribution such that at least about 60 weight percent of the particles lie within 50 percent of the equivalent discrete particle average spherical diameter, which when utilized as a filler in the manufacture of paper, results in a paper product that demonstrates a significant improvement in performance with respect to the optical properties of the paper over any previously made paper utilizing other forms of calcium carbonate as the filler material.
  • an alkali metal hydroxide preferably sodium hydroxide
  • Fig. 1 shows the specific surface area over time of samples of ultrafine precipitated calcium carbonate prepared according to both the accelerated heat-aging process and the conventional heat-aging process.
  • Fig. 2 is a particle size distribution curve of rhombohedral calcium carbonate showing the narrow size distribution.
  • Fig. 3 is a photomicrograph of the crystal morphology of particles of precipitated calcium carbonate heat-aged by the accelerated heat-aging process.
  • Fig. 4 is a photomicrograph of the industry standard non-heat-aged precipitated calcium carbonate having a scalenohedral rosette structure.
  • Fig. 5 is a comparison of pigment scattering coefficient in handsheets versus the percent filler content for various forms of heat-aged ultrafine precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 6 is a comparison of brightness in handsheets versus the percent filler content for various forms of heat-aged ultrafine precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 7 is a comparison of handsheet opacity versus the percent filler content for various forms of heat - aged ultrafine precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 8 shows handsheet opacity versus specific surface area for various heat-aged ultrafine precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 9 shows pigment scattering coefficient versus specific surface area for various heat-aged ultrafine precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 10 is a transmission electron micrograph of non-heat-aged ultrafine precipitated calcium carbonate showing initial crystal morphology before heat-aging.
  • Fig. 11 is a transmission electron micrograph of heat-aged ultrafine precipitated calcium carbonate showing the rhombohedral morphology.
  • Fig. 12 is a transmission electron micrograph of non-heat-aged scalenohedral precipitated calcium carbonate.
  • Fig. 13 is a transmission electron micrograph of heat-aged scalenohedral precipitated calcium carbonate showing the prismatic morphology.
  • Fig. 14 shows pigment scattering coefficient versus percent filler content in handsheets for various forms of heat-aged precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 15 shows opacity versus percent filler content in handsheets for various forms of heat-aged precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 16 shows brightness versus percent filler content in handsheets for various forms of heat-aged precipitated calcium carbonate and non-heat-aged precipitated calcium carbonate fillers.
  • Fig. 17 shows specific surface area versus time for various heat-aged ultrafines, heat-aged at various temperatures.
  • Fig. 18 shows a comparison of the aging rates between 80°C and 200°C for the accelerated heat-aging process using hydrothermally aged and non-hydrothermally aged starting materials.
  • Fig. 19 is a photomicrograph of hydrothermally heat-aged ultrafine precipitated calcium carbonate showing the rhombohedral morphology.
  • the crystal morphology of calcium carbonate is rearranged from an initial morphology having a surface area of greater than about 15 m2/g and an average discrete particle size of from about 0.01 to about 0.8 microns, to a final morphology having a surface area of from about 3 to about 15 m2/g, and an average discrete particle size of from about 0.2 to about 0.9 microns.
  • average discrete particle size refers to the equivalent spherical diameter of an individual particle which can exist as an individual particle or as part of a cluster or agglomerate, as opposed to the equivalent spherical diameter of the cluster or agglomerate itself.
  • the process comprises the steps of initiating heat-aging of the calcium carbonate by heating it to an aging temperature of from about 40 to about 100°C; adjusting the pH of the calcium carbonate at the aging temperature to about 6.5, such as by addition of carbon dioxide; adding an alkali metal hydroxide to the calcium carbonate at the aging temperature to raise the pH to from about 9.5 to about 12.0; maintaining the calcium carbonate at the aging temperature for a sufficient time to cause the morphology of the calcium carbonate to rearrange to the final form; and terminating heat-aging to fix the morphology of the calcium carbonate in the final form.
  • the process can be applied to calcium carbonate either as precipitated calcium carbonate or as fine ground natural limestone.
  • the calcium carbonate can be in a form either as a dry powder, which is subsequently slurried, or as an aqueous slurry.
  • a slurry having about a 10 weight percent calcium carbonate solids content is preferred.
  • the alkali metal hydroxide can be a hydroxide of any metal from group IA of the periodic table. Sodium hydroxide is preferred. It has been found that calcium hydroxide is not effective for use in adjusting the pH of the calcium carbonate at the aging temperature. This is believed to be due to the presence of the calcium ions formed on dissociation of the calcium hydroxide inhibiting the dissolution of calcium carbonate, thus slowing the aging process.
  • the amount of alkali metal hydroxide added to the calcium carbonate is in an amount of from about 0.1 to about 15 weight percent, based on the dry weight of calcium carbonate.
  • the alkali metal hydroxide added to adjust the pH can be pure or an aqueous alkali metal hydroxide solution.
  • Sodium hydroxide is the preferred alkali metal hydroxide.
  • the length of time the calcium carbonate must be maintained at the aging temperature in order to recrystallise to the new morphology is determined by both the initial morphology of the calcium carbonate and the nature and extent of any impurities present in the calcium carbonate.
  • the aging time is as short as about 60 minutes.
  • the heat-aging time can be as long as 24 hours.
  • Heat-aging can be terminated by either reducing the temperature to below about 40°C; by reduction of the pH; or by a combination of temperature and pH reduction.
  • heat-aging does not occur or proceeds at such a slow rate as to be insignificant when the temperature is reduced to about 40°C or below.
  • the heat-aging process is also very pH sensitive and a reduction of the pH to below about 8.5 effectively halts heat-aging and further recrystallization of the calcium carbonate.
  • Termination of heat-aging by temperature reduction can be effected rapidly by quenching the calcium carbonate, such as by immersion in an ice bath.
  • Termination of heat-aging by pH reduction is effected by addition of CO2 or of a polybasic acid to the calcium carbonate.
  • the polybasic acid is preferably phosphoric acid.
  • Calcium carbonate can also be heat-aged according to further embodiments of the process of the present invention which utilize hydrothermal techniques.
  • heat-aging in a hydrothermal bomb under hydrothermal conditions of high temperature, up to about 300°C, and under elevated pressure, up to about 750 psi causes an acceleration of the aging process and reduction in the required aging time from the time required for conventional heat-aging, and even a further reduction in aging time from the time required for non-hydrothermal accelerated heat-aging at conditions of lower temperature and ambient pressure.
  • heat-aging crystal morphology rearrangement process is still further accelerated in another embodiment of the process of the present invention wherein heat-aging is initiated at a temperature of from about 40 to about 100°C, and the initial pH of the starting calcium carbonate is adjusted to about 6.5, followed by addition of an alkali metal hydroxide, preferably sodium hydroxide, to the calcium carbonate at the heat-aging temperature to raise the pH to from about 9.5 to about 12.0, as in the non-hydrothermal accelerated heat-aging process of the present invention, and the calcium carbonate is then hydrothermally-aged in a hydrothermal bomb under hydrothermal conditions in which the bomb is pressurized to a pressure up to about 750 psi and the temperature in the bomb is then raised to the hydrothermal temperature at the bomb pressure, of up to about 300°C, at which conditions even more rapid rearrangement of the calcium carbonate crystal morphology occurs, resulting in an even shorter overall heat-aging time.
  • an alkali metal hydroxide preferably sodium hydroxide
  • any heat-aged calcium carbonate having the desired physical properties is effective, that produced according to the accelerated heat-aging process and the hydrothermal-aging process of the present invention, is highly desirable in that it is fast and economical to produce on a large scale in the quantities required for papermaking.
  • Precipitated calcium carbonate having less than 0.1 micron particle size referred to herein as "ultrafine", and a surface area of from about 25 to about 40 m2/g, was endpointed at pH of 6.7 to eliminate as much Ca(OH)2 as possible.
  • the product was screened to eliminate impurities, and 2400g of the product in a 10% by weight slurry was heated to 80°C. At 80°C, the pH of the slurry was again brought down to 6.7 with carbon dioxide, and 48g of sodium hydroxide was added to the slurry (2% by weight) to bring the pH up to an optimum aging pH of 10.9 - 11.1. Within one hour, the viscosity increased approximately 40-fold. Samples were taken every hour for surface area determination.
  • EXAMPLE 2 Uniqueness of particle morphology by accelerated heat-aging.
  • Figure 3 is a photomicrograph of the crystal morphology of particles heat-aged by the accelerated heat-aging process of this invention. This figure should be compared to Figure 4 which is a photomicrograph of the crystal morphology of non-heat-aged precipitated calcium carbonate having a scalenohedral rosette structure, which was heretofore the best known filler for achieving enhanced optical properties in paper.
  • EXAMPLE 3 Comparison of particle morphologies for different precursors.
  • EXAMPLE 4 Optimum accelerated heat-aging temperature.
  • a batch of ultrafine precipitated calcium carbonate (surface area 38 m2/g) was synthesized without additives and endpointed at pH 8.0.
  • a sample of this material was slurried to a 10% by weight solids content and 1800 ml of the slurry was placed into a 4 liter PARR hydrothermal bomb. The temperature was raised to 200°C at 500 psi, within one hour, held at 200°C for one hour and cooled for a total aging time of 2.5 hours.
  • the surface area of the product was 15.7 m2/g, which would have taken 7 hours to attain under conventional heat-aging conditions.
  • EXAMPLE 6 Hydrothermal-aging via accelerated aging process.
  • a batch of ultrafine precipitated calcium carbonate (surface area 38 m2/g) was divided into two portions, A and B.
  • Portion A was aged by the method described in Example 1.
  • Portion B was treated in a similar manner as portion A, as described in Example 1, up to and including the point were the sample was heated to 80°C and NaOH was added.
  • portion B was placed into a 4 liter PARR hydrothermal bomb where the temperature was raised to 200°C at 500 psi.
  • Portion B was kept at these conditions for 1 - 1.5 hours at which point the material was quenched to room temperature to prevent further aging.
  • Figure 18 shows the comparison of the aging rates between 80°C and 200°C where it can be seen that a decrease in surface area occurs at a much faster rate when the starting material is hydrothermally-aged.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Nanotechnology (AREA)
  • Physics & Mathematics (AREA)
  • Composite Materials (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
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EP95118361A 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat Revoked EP0703193B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US493075 1990-03-13
US07/493,075 US5269818A (en) 1990-03-13 1990-03-13 Rhombohedral calcium carbonate and accelerated heat-aging process for the production thereof
EP91301797A EP0447094B1 (de) 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat und beschleunigtes Alternverfahren in Wärme zur Herstellung davon

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
EP91301797.6 Division 1991-03-05
EP91301797A Division EP0447094B1 (de) 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat und beschleunigtes Alternverfahren in Wärme zur Herstellung davon

Publications (3)

Publication Number Publication Date
EP0703193A2 true EP0703193A2 (de) 1996-03-27
EP0703193A3 EP0703193A3 (de) 1996-06-05
EP0703193B1 EP0703193B1 (de) 1998-05-06

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ID=23958798

Family Applications (3)

Application Number Title Priority Date Filing Date
EP95118362A Expired - Lifetime EP0703315B1 (de) 1990-03-13 1991-03-05 Verfahren zur Verbesserung der optischen Eigenschaften von Papier
EP95118361A Revoked EP0703193B1 (de) 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat
EP91301797A Expired - Lifetime EP0447094B1 (de) 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat und beschleunigtes Alternverfahren in Wärme zur Herstellung davon

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP95118362A Expired - Lifetime EP0703315B1 (de) 1990-03-13 1991-03-05 Verfahren zur Verbesserung der optischen Eigenschaften von Papier

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP91301797A Expired - Lifetime EP0447094B1 (de) 1990-03-13 1991-03-05 Rhombohedrisches Calciumcarbonat und beschleunigtes Alternverfahren in Wärme zur Herstellung davon

Country Status (10)

Country Link
US (3) US5269818A (de)
EP (3) EP0703315B1 (de)
JP (1) JP3417954B2 (de)
KR (1) KR930001214B1 (de)
AU (2) AU7283891A (de)
BR (1) BR9100979A (de)
CA (1) CA2038009C (de)
DE (3) DE69128730T2 (de)
ES (3) ES2112602T3 (de)
FI (1) FI100722B (de)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000058217A1 (en) * 1999-03-31 2000-10-05 Minerals Technologies Inc. Process for the preparation of discrete particles of calcium carbonate
EP1586704A1 (de) * 2004-04-16 2005-10-19 SOLVAY (Société Anonyme) Verwendung von ultrafeine Kalziumkarbonatpartikeln zur Papierherstellung
EP1795502A1 (de) * 2005-12-12 2007-06-13 SOLVAY (Société Anonyme) Gefällte Calciumcarbonatteilchen, Verfahren zu deren Herstellung und deren Verwendung als Füllstoffe

Families Citing this family (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2157292A (en) * 1991-06-04 1993-01-08 Minerals Technologies Inc. Precipitated calcium carbonate particles from basic calcium carbonate
JPH07509684A (ja) * 1992-04-03 1995-10-26 ミネラルズ・テクノロジーズ・インコーポレーテッド クラスター状沈降炭酸カルシウム粒子
US5853686A (en) * 1993-08-10 1998-12-29 State Of Oregon Acting By And Through The Oregon State Board Of Higher Education On Behalf Of The University Of Oregon Calcium carbonates of altered crystal habit or morphology and methods for producing same
US5665205A (en) * 1995-01-19 1997-09-09 International Paper Company Method for improving brightness and cleanliness of secondary fibers for paper and paperboard manufacture
US5643631A (en) * 1995-03-17 1997-07-01 Minerals Tech Inc Ink jet recording paper incorporating novel precipitated calcium carbonate pigment
GB9520703D0 (en) * 1995-10-10 1995-12-13 Ecc Int Ltd Paper coating pigments and their production and use
US5741471A (en) * 1995-12-05 1998-04-21 Minerals Technologies Inc. Process for the preparation of discrete particles of calcium carbonate
US5830318A (en) * 1996-10-25 1998-11-03 Schweitzer-Mauduit International, Inc. High opacity tipping paper
US5888348A (en) * 1996-11-14 1999-03-30 Schweitzer-Mauduit International, Inc. Method for controlling the permeability of a paper
US5730840A (en) * 1996-11-14 1998-03-24 Schwietzer-Mauduit Inernational, Inc. Cigarette paper with improved ash characteristics
US6823872B2 (en) * 1997-04-07 2004-11-30 Schweitzer-Mauduit International, Inc. Smoking article with reduced carbon monoxide delivery
US5893372A (en) * 1997-04-07 1999-04-13 Schweitzer Maudit International, Inc. High opacity wrapping paper
US6305382B1 (en) 1997-04-07 2001-10-23 Schweitzer-Mauduit International, Inc. Reduced basis weight cigarette paper
US5921249A (en) * 1997-07-14 1999-07-13 Schweitzer-Mauduit International, Inc. High and low porosity wrapping papers for smoking articles
US6100232A (en) * 1998-03-02 2000-08-08 The Procter & Gamble Company Process for making a granular detergent composition containing a selected crystalline calcium carbonate builder
US6251356B1 (en) 1999-07-21 2001-06-26 G. R. International, Inc. High speed manufacturing process for precipitated calcium carbonate employing sequential perssure carbonation
US6440209B1 (en) 2000-02-09 2002-08-27 Engelhard Corpoartion Composite pigments comprising in-situ precipitated metal carbonate crystals
DE10007484C2 (de) 2000-02-18 2001-12-13 Schoeller Felix Jun Foto Schichtträger für Aufzeichnungsmaterialien
US6568403B2 (en) 2000-06-22 2003-05-27 Schweitzer-Mauduit International, Inc. Paper wrapper for reduction of cigarette burn rate
US7048900B2 (en) * 2001-01-31 2006-05-23 G.R. International, Inc. Method and apparatus for production of precipitated calcium carbonate and silicate compounds in common process equipment
JP3484425B2 (ja) * 2001-03-14 2004-01-06 花王株式会社 歯磨剤
US6592837B2 (en) 2001-04-20 2003-07-15 Carbominerals Narrow size distribution ground calcium carbonate compositions
DE10357437A1 (de) * 2003-12-09 2005-07-07 Voith Paper Patent Gmbh Verfahren zum Beladen einer Faserstoffsuspension und Anordnung zur Durchführung des Verfahrens
US20070167531A1 (en) * 2004-02-05 2007-07-19 Preston David J Natural particulate carbonate
US20060060317A1 (en) * 2004-09-20 2006-03-23 International Paper Company Method to reduce back trap offset print mottle
US20070181275A1 (en) * 2005-04-14 2007-08-09 Solvay (Socete Anonyme) Use of calcuim carbonate particles in papermaking
EP1999083B1 (de) 2006-03-24 2013-01-23 NewPage Wisconsin System Inc. Papier und beschichtungsmedium zum mehrzweckdrucken
JP4801478B2 (ja) * 2006-03-27 2011-10-26 日本製紙株式会社 ブロークパルプの処理方法
US7468101B2 (en) 2006-08-17 2008-12-23 Specialty Minerals (Michigan) Inc. UV varnish gloss performance using novel pigment and process for making same
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EP1586704A1 (de) * 2004-04-16 2005-10-19 SOLVAY (Société Anonyme) Verwendung von ultrafeine Kalziumkarbonatpartikeln zur Papierherstellung
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US5269818A (en) 1993-12-14
CA2038009C (en) 1996-12-24
KR910016628A (ko) 1991-11-05
ES2117823T3 (es) 1998-08-16
ES2112602T3 (es) 1998-04-01
JP3417954B2 (ja) 2003-06-16
DE69128730T2 (de) 1998-07-16
EP0703193B1 (de) 1998-05-06
FI911211A0 (fi) 1991-03-12
FI100722B (fi) 1998-02-13
JPH05319816A (ja) 1993-12-03
EP0447094B1 (de) 1996-09-18
DE69122146D1 (de) 1996-10-24
DE69129377D1 (de) 1998-06-10
FI911211A (fi) 1991-09-14
CA2038009A1 (en) 1991-09-14
US5215734A (en) 1993-06-01
EP0703315A2 (de) 1996-03-27
BR9100979A (pt) 1991-11-05
EP0447094A1 (de) 1991-09-18
EP0703315B1 (de) 1998-01-14
AU7283891A (en) 1991-10-10
DE69122146T2 (de) 1997-04-03
EP0703315A3 (de) 1996-06-26
DE69129377T2 (de) 1998-11-19
ES2092545T3 (es) 1996-12-01
AU666539B2 (en) 1996-02-15
DE69128730D1 (de) 1998-02-19
US5296002A (en) 1994-03-22
KR930001214B1 (ko) 1993-02-22
EP0703193A3 (de) 1996-06-05
AU3870093A (en) 1993-08-05

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